P
US4309282AExpiredUtilityPatentIndex 89

Process of phosphate ore beneficiation in the presence of residual organic polymeric flocculants

Assignee: AMERICAN CYANAMID COPriority: Apr 14, 1980Filed: Apr 14, 1980Granted: Jan 5, 1982
Est. expiryApr 14, 2000(expired)· nominal 20-yr term from priority
Inventors:SMITH JR EUGENE LPOULOS ANDREW CELLWANGER RICHARD E
B03D 2201/002B03D 1/016B03D 2201/02B03D 1/008B03D 1/021B03D 2203/06B03D 1/012
89
PatentIndex Score
31
Cited by
9
References
6
Claims

Abstract

Froth flotation of phosphate ore in the presence of residual organic polymeric flocculants is improved in recovery when a collector comprising a fatty acid derived from vegetable or mineral oils and a surface active agent is employed.

Claims

exact text as granted — not AI-modified
What is claimed is: 
     
       1. A process for the froth flotation of phosphate values from an aqueous ore pulp containing about 0.1 to 5 parts per million of residual organic polymer flocculants which comprises: conditioning said ore pulp with from about 0.1 to 5.0 pounds of collector per ton of ore, said collector comprising, in combination, from about 99.0 to 1.0 weight percent of a fatty acid derived from vegetable or animal oils and, correspondingly, from about 1.0 to 99.0 weight percent of a surface active agent wherein the surface active agent is either a partial polycarboxylic acid ester of the general structure: ##STR13## wherein R 2  is a linear or branched radical having from 8 to 23 carbon atoms, inclusive, n is an integer of from 0 to 8 inclusive, p is an integer of from 0 to 8 inclusive, wherein n+p is equal to or greater than (1) and R 1  is a bivalent grouping selected from --CH 2  --m wherein m is an integer of 1 to 6, --CH═CH, ##STR14## --C 6  H 8  --, and C 6  H 10  --, or is a sulfosuccinamate of the general structure: ##STR15## wherein R 2  is a linear or branched, saturated or unsaturated radical having from 8 to 23 carbon atoms, inclusive, and X is selected from the group consisting of hydrogen, sodium, potassium and ammonium and thereafter froth floating the phosphate values. 
     
     
       2. The process of claim 1 wherein from about 0.5 to about 2.0 pounds of collector per ton of ore is employed. 
     
     
       3. The process of claim 1 wherein the collector comprises from about 95.0 to 80.0 weight percent of a fatty acid and, correspondingly, from about 5.0 to 20.0 weight percent of a surface active agent. 
     
     
       4. The process of claim 1 wherein the fatty acid employed in the collector is derived from tall oil. 
     
     
       5. The process of claim 1 wherein the partial polycarboxylic acid ester employed in the collector is one in which R 2  is a linear or branched aliphatic radical having 11 to 15 carbon atoms, inclusive. 
     
     
       6. The process of claim 1 wherein the partial polycarboxylic acid ester employed in the collector is of the structure: ##STR16##

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